Heat pump-based water harvesting systems
Water harvesting systems and methods of making and using such water harvesting systems, for capturing water from surrounding air using configurations that reduce overall energy costs and improves water harvesting cycle efficiency in the water harvesting system. In particular embodiments, the water harvesting system can be configured for dehumidification-humidification of air, and a method in the water harvesting system for dehumidification-humidification to control moisture level in the air conditioned by the water harvesting system. The systems and methods use sorbent materials, such as metal-organic frameworks, to adsorb water from the air. The systems and methods desorb this water in the form of water vapor, and the water vapor can be condensed into liquid water and collected to dehumidify air conditioned by the water harvesting system. The collected liquid water can be sprayed to humidify air conditioned by the water harvesting system.
1. An atmospheric water harvesting system, comprising:
a heat pump having a hot side heat exchanger and a cold side heat exchanger;
an adsorption unit comprising a plurality of sorbent modules, wherein each of said plurality of sorbent modules contains one or more sorbents, said adsorption unit disposed physically separate from said heat pump;
a desorption chamber connected to or positioned in close proximity to said hot side heat exchanger of said heat pump, said desorption chamber is configured to operate at a desorption temperature, wherein one or more of said plurality of sorbent modules disposed in said desorption chamber releases water vapor from said one or more sorbents at said desorption temperature; and
a condensation chamber encompassing or positioned in close proximity to said cold side heat exchanger of said heat pump, wherein said condensation chamber is configured to operate at a condensation temperature, wherein said condensation chamber is fluidically coupled to said desorption chamber to receive said water vapor, said water vapor condenses within said condensation chamber at said condensation temperature, wherein said desorption temperature and said condensation temperature each independently controlled to achieve the lowest energy consumption per liter of water.
2. The system of claim 1 , further comprising at least one recirculation fan configured to: (i) transfer heat from said hot side heat exchanger to said sorbent module in said desorption chamber, and (ii) drive desorption of water from said sorbent module to achieve a higher concentration of water in said desorption chamber.
3. The system of claim 1 , further comprising a secondary hot side heat exchanger.
4. The system of claim 1 , further comprising one or more control components to regulate said heat pump.
5. The system of claim 1 , wherein the system further comprises a water collection tank.
6. The system of claim 1 , wherein one or more sorbents comprises a metal-organic framework.
7. The system of claim 6 , wherein said metal-organic framework has an isotherm step of about 20% relative humidity at about 25° C.
8. The system of claim 7 , wherein said desorption temperature occurs in a range of about 130° C. to about 140° C., and wherein said condensation temperature occurs in a range of about 85° C. to about 95° C.
9. The system of claim 6 , wherein said metal-organic framework has an isotherm step of about 40% relative humidity at about 25° C.
10. The system of claim 9 , wherein said desorption temperature occurs in a range of about 115° C. to about 125° C., and wherein said condensation temperature occurs in a range of about 85° C. to about 95° C.
11. The system of claim 6 , wherein said metal-organic framework has an isotherm step of about 60% relative humidity at about 25° C.
12. The system of claim 11 , wherein said desorption temperature occurs in a range of about 100° C. to about 110° C., and wherein said condensation temperature occurs in a range of about 85° C. to about 95° C.
13. A system, comprising:
a heat pump having a hot side heat exchanger and a cold side heat exchanger;
an adsorption unit comprising a sorbent module, said sorbent module contains one or more sorbents, said adsorption unit disposed physically separate from said heat pump;
a desorption chamber connected to or positioned in close proximity to said hot side heat exchanger of said heat pump;
a condensation chamber encompassing or positioned in close proximity to said cold side heat exchanger of said heat pump;
a water collection tank connected to said condensation chamber, said water collection tank configured to collect water condensed from said condensation chamber;
a water pump connected to said water collection tank, configured to receive said water from said collection tank;
a sprayer connected to said water pump and positioned in proximity to an indoor outlet;
a bypass unit positioned in proximity to the adsorption unit, configured to transfer air from an outdoor inlet or indoor inlet;
an adsorption fan positioned in proximity to said adsorption unit and said bypass unit to transfer air from said outdoor inlet or said indoor inlet into the adsorption unit and the bypass unit;
an indoor/outdoor inlet damper configured to control flow of air into the adsorption unit and the bypass unit from said outdoor inlet or said indoor inlet;
an adsorption damper configured to direct a portion of airflow into the adsorption unit and a portion of airflow into the bypass unit; and
an indoor/outdoor outlet damper configured to control flow of air out of the adsorption unit and the bypass unit into an outdoor outlet or an indoor outlet,
said system adapted to switch operation between a first mode to dehumidify said air from said outdoor inlet to said indoor outlet, a second mode to humidify air from outdoor inlet to indoor outlet, a third mode to dehumidify air recirculated from said indoor inlet to said indoor outlet, and fourth mode to humidify air recirculated from said indoor inlet to said indoor outlet.
14. The system of claim 13 , wherein in said first mode:
said indoor/outdoor inlet damper closes said indoor inlet and opens said outdoor inlet, to transfer air from said outdoor inlet to said adsorption unit and to said bypass unit;
said adsorption damper controls said portion of airflow into the adsorption unit and said portion of airflow into said bypass unit;
said indoor/outdoor outlet damper closes said outdoor outlet and opens said indoor outlet to transfer dehumidified air from said adsorption unit through said indoor outlet;
a transfer mechanism transfers said sorbent module at least partially saturated with water from said adsorption unit into said desorption chamber, wherein water desorbs from said one or more sorbents contained in said sorbent module, wherein said water desorbed from said one or more sorbents condenses in said condensation chamber;
said water condensed in said condensation chamber collects in said water collection tank, wherein at least a portion of said water collected in said water collection tank transferred to a drain; and
said water pump remains in an off condition.
15. The system of claim 13 , wherein in said second mode:
said indoor/outdoor inlet damper closes an indoor inlet and opens said outdoor inlet to transfer air from said outdoor inlet to said adsorption unit and to said bypass unit;
said adsorption damper closes said bypass unit and opens said adsorption unit;
said indoor/outdoor outlet damper partially opens said outdoor outlet and said indoor outlet to transfer dehumidified air from said adsorption through said indoor outlet and through said outdoor outlet;
a transfer mechanism transfers said sorbent module at least partially saturated with water from said adsorption unit into said desorption chamber, wherein water desorbs from said one or more sorbents contained in said sorbent module, wherein said water desorbed from said one or more sorbents condenses in said condensation chamber; and
said water condensed in said condensation chamber collects in said water collection tank, wherein at least a portion of said water collected in said water collection tank transferred to a drain;
at least a portion of said water in water collection tank transferred by said water pump to said sprayer to humidify air transferred through the indoor outlet, said drain remains in an off condition.
16. The system of claim 13 , wherein in said third mode:
said indoor/outdoor inlet damper closes said outdoor inlet and opens said indoor inlet to transfer air from said indoor inlet to said adsorption unit and to said bypass unit;
said adsorption damper controls said portion of airflow into the adsorption unit and said portion of airflow into said bypass unit;
said indoor/outdoor outlet damper closes said outdoor outlet and opens said indoor outlet, to transfer dehumidified air from said adsorption unit through said indoor outlet;
a transfer mechanism transfers said sorbent module at least partially saturated with water from said adsorption unit into said desorption chamber, wherein water desorbs from said one or more sorbents contained in said sorbent module, wherein said water desorbed from said one or more sorbents condenses in said condensation chamber;
said water condensed in said condensation chamber collects in said water collection tank, wherein at least a portion of said water collected in said water collection tank transferred to a drain; and
said water pump remains in an off condition.
17. The system of claim 13 , wherein in said fourth mode, said system operates in a first configuration and subsequently said system operates in a second configuration, wherein said system in first configuration:
said indoor/outdoor inlet damper closes said indoor inlet and opens said outdoor inlet, to transfer air to said adsorption unit and said bypass unit;
said adsorption damper closes said bypass unit and opens said adsorption unit;
said indoor/outdoor outlet damper closes said indoor outlet and opens said outdoor outlet to transfer air from said adsorption unit through said outdoor outlet;
a transfer mechanism transfers said sorbent module at least partially saturated with water from said adsorption unit into said desorption chamber, wherein water desorbs from said one or more sorbents contained in said sorbent module, wherein said water desorbed from said one or more sorbents condenses in said condensation chamber;
said water condensed in said condensation chamber collects in said water collection tank, said water pump remains in an off condition, and
wherein said system in said second configuration:
said indoor/outdoor inlet damper closes said outdoor inlet and opens said indoor inlet, to allow air to transfer to said absorbent unit and said bypass unit;
said adsorption damper closes said adsorption unit and opens said bypass unit;
said indoor/outdoor outlet damper closes said outdoor outlet and opens said indoor outlet to transfer air from said bypass unit through said indoor outlet;
at least a portion of said water in water collection tank transferred by said water pump to said sprayer to humidify air transferred through the indoor outlet, said drain remains in an off condition.
18. A system, comprising:
a heat pump having a hot side heat exchanger and a cold side heat exchanger;
an adsorption unit comprising a sorbent module, said sorbent module contains one or more sorbents, said adsorption unit disposed physically separate from said heat pump;
a desorption chamber connected to or positioned in close proximity to said hot side heat exchanger of said heat pump;
a condensation chamber encompassing or positioned in close proximity to said cold side heat exchanger of said heat pump; and
at least one desorption-condenser recirculation fan configured to (i) transfer water desorbed from said sorbent module in said desorption chamber to said condensation chamber, and (ii) recirculate remaining desorbed water from said sorbent module in the condensation chamber back into the desorption chamber.
19. A system, comprising:
a heat pump having a hot side heat exchanger and a cold side heat exchanger;
an adsorption unit comprising a sorbent module, said sorbent module contains one or more sorbents, said adsorption unit disposed physically separate from said heat pump;
a desorption chamber connected to or positioned in close proximity to said hot side heat exchanger of said heat pump;
a condensation chamber encompassing or positioned in close proximity to said cold side heat exchanger of said heat pump; and
a transfer mechanism configured to (i) transfer said sorbent module at least partially saturated with water from said adsorption unit into said desorption chamber, and (ii) transfer said sorbent module at least partially desorbed of said water from said desorption chamber back to said adsorption unit.